CN104613576A - Multistage direct evaporation cooling machine set - Google Patents
Multistage direct evaporation cooling machine set Download PDFInfo
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- CN104613576A CN104613576A CN201510003672.2A CN201510003672A CN104613576A CN 104613576 A CN104613576 A CN 104613576A CN 201510003672 A CN201510003672 A CN 201510003672A CN 104613576 A CN104613576 A CN 104613576A
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- water
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- multistage direct
- cooling unit
- spray chamber
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
- B01D47/06—Spray cleaning
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F5/00—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater
- F24F5/0007—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning
- F24F5/0035—Air-conditioning systems or apparatus not covered by F24F1/00 or F24F3/00, e.g. using solar heat or combined with household units such as an oven or water heater cooling apparatus specially adapted for use in air-conditioning using evaporation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/144—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by dehumidification only
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Separation Of Particles Using Liquids (AREA)
Abstract
The invention relates to a multistage direct evaporation cooling machine set. The multistage direct evaporation cooling machine set solves the problems that irrational utilization of cooling air existing in the prior evaporation cooling machine set. The multistage direct evaporation cooling machine set comprises a machine set shell, an air channel, a circulating water tank, spray chambers, gas channels, a first water-cooling atomization mechanism, a flow-guidance filter structure and a dehumidification device, a material-filling area is arranged in the gas channels, a second water-cooling atomization mechanism is arranged over the material-filling area, surface heat exchangers are respectively arranged in the air channel, one end of each surface heat exchanger is provided with a condensate water inlet, the other end is communicated with a middle heat exchanger, and the middle heat exchangers are provided with condensate water outlets. The multistage direct evaporation cooling machine set has the advantages that the remain cooling capacity taken by the air is recycled, during the temperature of the air reduction the dust-cleaning is realized, the effect of dehumidification is provided, the temperature of the air reduced again, and de-mineralized water attached to the dehumidification device returns to the circulating water tank. Accordingly, the de-mineralized water can be recycled and the goal of saving water is achieved.
Description
Technical field
The invention belongs to technical field of refrigeration equipment, relate to a kind of dust arrester, especially relate to a kind of multistage direct evaporating-cooling unit.
Background technology
At torridity summer, most phenomenon using the power plant of air cooling heat radiator all to occur large load high back pressure, this has a huge impact the economical production in power plant, therefore needs to seek more excellent auxiliary equipment to improve this phenomenon, aestivates for power plant safety.Compared with traditional mechanical refrigeration, evaporation cooling technique effect in refrigeration is better.Mostly the version of current evaporation cooling high-temperature handpiece Water Chilling Units is tube type indirect evaporative cooler or aerial cooler and direct evaporative cooler to be composited.And the efficiency of tube type indirect evaporative cooler and direct evaporative cooler changes along with outdoor weather condition, the stability of high temperature cold water is produced in impact, moreover shower water is directly after packing section and air carry out heat and wet treatment, the air draft that temperature is lower is directly discharged in the middle of air, do not obtain Appropriate application, independent employing direct evaporating-cooling technology prepares cold water, the high temperature refrigerant water produced is generally higher than the wet-bulb temperature of outdoor air, the requirement of sensible heat end can not be met, and efficiency of damp and hot exchanging is low, irreversible loss is larger, can not make full use of dry air, refrigeration reduces greatly, also the cold self prepared well is not utilized.
In order to solve prior art Problems existing, people have carried out long-term exploration, propose solution miscellaneous.Such as, Chinese patent literature discloses a kind of closed-type negative-pressure evaporative cooling handpiece Water Chilling Units [application number: 201310163751.0] applying hydrodynamic draught fan, include machine unit shell, the two side that machine unit shell is relative is provided with air inlet, there is the direct evaporative cooler of band cooling coil at middle part in machine unit shell, direct evaporative cooler both sides with cooling coil are respectively symmetrically arranged with the standpipe type indirect evaporation cooler of a band filler, filter and aerial cooler is disposed with between the standpipe type indirect evaporation cooler of the band filler of air inlet and homonymy, with the direct evaporative cooler of cooling coil, connected by pipe network between the standpipe type indirect evaporation cooler of two band fillers and two aerial coolers.
Such scheme to some extent solves the problem of existing evaporative cooling unit cooling effect difference, but the program still fundamentally cannot solve the problem that cooled air does not have Appropriate application.
Summary of the invention
The object of the invention is for the problems referred to above, provide a kind of simple and reasonable, can by the multistage direct evaporating-cooling unit of cooled gas to the diffusion that condensed water is lowered the temperature.
For achieving the above object, present invention employs following technical proposal: this multistage direct evaporating-cooling unit, comprise machine unit shell, described machine unit shell upper end is provided with air channel, lower end is provided with cyclic water tank, the inner both sides of described machine unit shell are respectively equipped with spray chamber, formed between described spray chamber and vertically arrange and the gas passage be connected with air channel, it is characterized in that, the first water-cooled atomising mechanism that can produce water fog particle is provided with in described spray chamber, be provided with between spray chamber and cyclic water tank and water fog particle can be collected and filter the water conservancy diversion filtration being back to cyclic water tank, dehydrating unit is provided with between described spray chamber and gas passage, packing area is provided with in gas passage, the second water-cooled atomising mechanism is provided with above described packing area, the surface exchanger being positioned at both sides, gas passage end is respectively equipped with in described air channel, and described surface exchanger one end is provided with condensed water import, the other end is connected with the Intermediate Heat Exchanger be arranged between packing area and the second water-cooled atomising mechanism, and described Intermediate Heat Exchanger is provided with condensation-water drain.
In this structure, first water-cooled atomising mechanism carries out the first cooling to high temperature air, water fog particle can be collected and filter and be back to cyclic water tank by water conservancy diversion filtration simultaneously, for follow-up unit, through the high temperature air of once lowering the temperature through dehydrating unit, dehydrating unit is by the moisture in absorbed air, take away the heat in air simultaneously, air secondary is lowered the temperature, the moisture that dehydrating unit adsorbs will be got back in cyclic water tank, for follow-up unit, the air of reducing temperature twice is first through filler, the moisture film formed with filling surface carries out hot moisture exchange, air is lowered the temperature again, humidity increases, surface exchanger is positioned over the outlet in air channel, and the air having carried out heat exchange with process and Intermediate Heat Exchanger carries out exchange heat, makes the high-temperature condensation water one in surface exchanger obtain precooling, enter described Intermediate Heat Exchanger again after high-temperature condensation water precooling in surface exchanger, the air of lowering the temperature with moisture film and three times carries out heat exchange, obtains reducing temperature twice, and then gets back to electric power supply plant use in condensed water in power plant system.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, described water conservancy diversion filtration comprises the deflector be inclined in spray chamber, described deflector one end is connected with dehydrating unit, form the pod apertures be connected with cyclic water tank between the other end with machine unit shell, in pod apertures, be provided with filter.Namely the water smoke having adsorbed air plankton drops on deflector, then through filter, filter will filter out impurity, and water quality is improved.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, the first described water-cooled atomising mechanism comprises the water circulating pump be connected with cyclic water tank, and described water circulating pump is connected with some the first shower nozzles be arranged on deflector respectively, and the first described shower nozzle is towards in spray chamber.First shower nozzle ejection water smoke, by the impurity parcel in high temperature air, falls under gravity.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, the second described water-cooled atomising mechanism comprises the water-locator be arranged on above Intermediate Heat Exchanger, and described water-locator is connected with water circulating pump, and on water-locator, be provided with some the second shower nozzles towards Intermediate Heat Exchanger.Namely the second shower nozzle ejection water smoke forms moisture film thus lowers the temperature to the condensed water in Intermediate Heat Exchanger on Intermediate Heat Exchanger.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, be provided with the baffle plate of horizontally set above described water-locator, described baffle plate is provided with negative pressure mechanism.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, described negative pressure mechanism comprises and is arranged on baffle plate and is positioned at the blower fan of gas passage upper end.Blower fan makes machine unit shell inside form negative pressure, promotes the flowing of evaporation of water and air.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, described packing area is put together by some bullets set gradually, and the diameter of described bullet near one end of Intermediate Heat Exchanger to the diameter of the other end diminishes gradually.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, between adjacent two bullets, form air-flow buffer district, and the diameter of described upper end, air-flow buffer district to the diameter of lower end becomes large gradually.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, described dehydrating unit is the platy structure be obliquely installed, and forms the bottom-up air flow guiding district diminished gradually of diameter between described dehydrating unit and packing area.Obviously, this structure is convenient to the circulation of air.
At above-mentioned multistage direct evaporating-cooling unit, it is characterized in that, described machine unit shell outer circumferential is provided with some shutters be connected with spray chamber.
Compared with prior art, the advantage of this multistage direct evaporating-cooling unit is: the residue cold 1, air can taken away reclaims, and serves the effect reducing the second investment, economize energy; 2, while to air cooling-down, realize dedusting, also reduce the possibility of described water-locator top nozzle blocking; 3, there is the effect of dehumidifying, air lowered the temperature again, obtain temperature lower, air that relative humidity is less; The demineralized water be adsorbed on dehydrating unit is got back in cyclic water tank, demineralized water can be made to reuse, reach water-saving object.
Accompanying drawing explanation
Fig. 1 is structural representation provided by the invention.
In figure, machine unit shell 1, gas passage 11, packing area 12, bullet 121, air-flow buffer district 122, air flow guiding district 123, shutter 13, air channel 2, cyclic water tank 3, spray chamber 4, first water-cooled atomising mechanism 5, water circulating pump 51, first shower nozzle 52, water conservancy diversion filtration 6, deflector 61, pod apertures 62, filter 63, dehydrating unit 7, second water-cooled atomising mechanism 8, water-locator 81, second shower nozzle 82, baffle plate 83, blower fan 84, surface exchanger 9, condensed water import 91, Intermediate Heat Exchanger 92, condensation-water drain 93.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the present invention will be further described in detail.
As shown in Figure 1, this multistage direct evaporating-cooling unit, comprise machine unit shell 1, machine unit shell 1 outer circumferential is provided with some shutters 13 be connected with spray chamber 4, machine unit shell 1 upper end is provided with air channel 2, lower end is provided with cyclic water tank 3, the inner both sides of machine unit shell 1 are respectively equipped with spray chamber 4, formed between spray chamber 4 and vertically arrange and the gas passage 11 be connected with air channel 2, the first water-cooled atomising mechanism 5 that can produce water fog particle is provided with in spray chamber 4, be provided with between spray chamber 4 and cyclic water tank 3 and water fog particle can be collected and filter the water conservancy diversion filtration 6 being back to cyclic water tank 3, dehydrating unit 7 is provided with between spray chamber 4 and gas passage 11, packing area 12 is provided with in gas passage 11, the second water-cooled atomising mechanism 8 is provided with above packing area 12, the surface exchanger 9 being positioned at both sides, gas passage 11 end is respectively equipped with in air channel 2, and surface exchanger 9 one end is provided with condensed water import 91, the other end is connected with the Intermediate Heat Exchanger 92 be arranged between packing area 12 and the second water-cooled atomising mechanism 8, and Intermediate Heat Exchanger 92 is provided with condensation-water drain 93, namely the first water-cooled atomising mechanism 5 pairs of high temperature airs in the present embodiment carry out the first cooling, water fog particle can be collected and filter and be back to cyclic water tank 3 by water conservancy diversion filtration 6 simultaneously, for follow-up unit, through the high temperature air of once lowering the temperature through dehydrating unit 7, dehydrating unit 7 is by the moisture in absorbed air, take away the heat in air simultaneously, air secondary is lowered the temperature, the moisture that dehydrating unit 7 adsorbs will be got back in cyclic water tank 3, for follow-up unit, the air of reducing temperature twice is first through packing area 12, the moisture film formed with filling surface carries out hot moisture exchange, air is lowered the temperature again, humidity increases, surface exchanger 9 is positioned over the outlet in air channel 2, and the air having carried out heat exchange with process and Intermediate Heat Exchanger 92 carries out exchange heat, makes the high-temperature condensation water one in surface exchanger 9 obtain precooling, enter described Intermediate Heat Exchanger 92 again after high-temperature condensation water precooling in surface exchanger 9, the air of lowering the temperature with moisture film and three times carries out heat exchange, obtains reducing temperature twice, and then gets back to electric power supply plant use in condensed water in power plant system.
Particularly, water conservancy diversion filtration 6 in the present embodiment comprises the deflector 61 be inclined in spray chamber 4, deflector 61 one end is connected with dehydrating unit 7, the pod apertures 62 be connected with cyclic water tank 3 is formed between the other end with machine unit shell 1, in pod apertures 62, be provided with filter 63, the water smoke namely having adsorbed air plankton drops on deflector 61, then through filter 63, filter 63 will filter out impurity, and water quality is improved.Further, here the first water-cooled atomising mechanism 5 comprises the water circulating pump 51 be connected with cyclic water tank 3, water circulating pump 51 is connected with some the first shower nozzles 52 be arranged on deflector 61 respectively, and the first shower nozzle 52 is towards in spray chamber 4, namely the first shower nozzle 52 sprays water smoke by the impurity parcel in high temperature air, falls under gravity.Preferably, here the second water-cooled atomising mechanism 8 comprises the water-locator 81 be arranged on above Intermediate Heat Exchanger 92, water-locator 81 is connected with water circulating pump 51, and on water-locator 81, be provided with some the second shower nozzles 82 towards Intermediate Heat Exchanger 92, namely the second shower nozzle 82 sprays water smoke and on Intermediate Heat Exchanger 92, forms moisture film thus lower the temperature to the condensed water in Intermediate Heat Exchanger 92.
Further, be provided with the baffle plate 83 of horizontally set above water-locator 81 here, baffle plate 83 is provided with negative pressure mechanism.Wherein, negative pressure mechanism comprises and is arranged on baffle plate 83 and is positioned at the blower fan 84 of gas passage 11 upper end, and namely blower fan 84 makes machine unit shell 1 inside form negative pressure, promotes the flowing of evaporation of water and air.
Preferably, packing area 12 is here put together by some bullets 121 set gradually, and the diameter of bullet 121 near one end of Intermediate Heat Exchanger 92 to the diameter of the other end diminishes gradually.Form air-flow buffer district 122 between adjacent two bullets 121, and the diameter of upper end, air-flow buffer district 122 to the diameter of lower end becomes large gradually.For the ease of the circulation of air, the platy structure of dehydrating unit 7 for being obliquely installed, and between dehydrating unit 7 and packing area 12, form the bottom-up air flow guiding district 123 diminished gradually of diameter.
Specific embodiment described herein is only to the explanation for example of the present invention's spirit.Those skilled in the art can make various amendment or supplement or adopt similar mode to substitute to described specific embodiment, but can't depart from spirit of the present invention or surmount the scope that appended claims defines.
Although more employ machine unit shell 1 herein, gas passage 11, packing area 12, bullet 121, air-flow buffer district 122, air flow guiding district 123, shutter 13, air channel 2, cyclic water tank 3, spray chamber 4, first water-cooled atomising mechanism 5, water circulating pump 51, first shower nozzle 52, water conservancy diversion filtration 6, deflector 61, pod apertures 62, filter 63, dehydrating unit 7, second water-cooled atomising mechanism 8, water-locator 81, second shower nozzle 82, baffle plate 83, blower fan 84, surface exchanger 9, condensed water import 91, Intermediate Heat Exchanger 92, term such as condensation-water drain 93 grade, but do not get rid of the possibility using other term.These terms are used to be only used to describe and explain essence of the present invention more easily; The restriction that they are construed to any one additional is all contrary with spirit of the present invention.
Claims (10)
1. a multistage direct evaporating-cooling unit, comprise machine unit shell (1), described machine unit shell (1) upper end is provided with air channel (2), lower end is provided with cyclic water tank (3), described machine unit shell (1) inner both sides are respectively equipped with spray chamber (4), formed between described spray chamber (4) and vertically arrange and the gas passage (11) be connected with air channel (2), it is characterized in that, the first water-cooled atomising mechanism (5) that can produce water fog particle is provided with in described spray chamber (4), be provided with between spray chamber (4) and cyclic water tank (3) and water fog particle can be collected and filter the water conservancy diversion filtration (6) being back to cyclic water tank (3), dehydrating unit (7) is provided with between described spray chamber (4) and gas passage (11), packing area (12) is provided with in gas passage (11), described top, packing area (12) is provided with the second water-cooled atomising mechanism (8), the surface exchanger (9) being positioned at gas passage (11) both sides, end is respectively equipped with in described air channel (2), and described surface exchanger (9) one end is provided with condensed water import (91), the other end is connected with the Intermediate Heat Exchanger (92) be arranged between packing area (12) and the second water-cooled atomising mechanism (8), and described Intermediate Heat Exchanger (92) is provided with condensation-water drain (93).
2. multistage direct evaporating-cooling unit according to claim 1, it is characterized in that, described water conservancy diversion filtration (6) comprises the deflector (61) be inclined in spray chamber (4), described deflector (61) one end is connected with dehydrating unit (7), form the pod apertures (62) be connected with cyclic water tank (3) between the other end with machine unit shell (1), in pod apertures (62), be provided with filter (63).
3. multistage direct evaporating-cooling unit according to claim 2, it is characterized in that, the first described water-cooled atomising mechanism (5) comprises the water circulating pump (51) be connected with cyclic water tank (3), described water circulating pump (51) is connected with some the first shower nozzles (52) be arranged on deflector (61) respectively, and described the first shower nozzle (52) is towards in spray chamber (4).
4. multistage direct evaporating-cooling unit according to claim 3, it is characterized in that, the second described water-cooled atomising mechanism (8) comprises the water-locator (81) being arranged on Intermediate Heat Exchanger (92) top, described water-locator (81) is connected with water circulating pump (51), and on water-locator (81), be provided with some the second shower nozzles (82) towards Intermediate Heat Exchanger (92).
5. multistage direct evaporating-cooling unit according to claim 4, is characterized in that, described water-locator (81) top is provided with the baffle plate (83) of horizontally set, and described baffle plate (83) is provided with negative pressure mechanism.
6. multistage direct evaporating-cooling unit according to claim 5, is characterized in that, described negative pressure mechanism comprises that to be arranged on baffle plate (83) upper and be positioned at the blower fan (84) of gas passage (11) upper end.
7. the multistage direct evaporating-cooling unit according to any one in claim 1-6, it is characterized in that, described packing area (12) is put together by some bullets (121) set gradually, and the diameter of described bullet (121) near one end of Intermediate Heat Exchanger (92) diminishes gradually to the diameter of the other end.
8. multistage direct evaporating-cooling unit according to claim 7, it is characterized in that, form air-flow buffer district (122) between adjacent two bullets (121), and the diameter of described air-flow buffer district (122) upper end to the diameter of lower end becomes large gradually.
9. multistage direct evaporating-cooling unit according to claim 7, it is characterized in that, described dehydrating unit (7) platy structure for being obliquely installed, and between described dehydrating unit (7) and packing area (12), form the bottom-up air flow guiding district (123) diminished gradually of diameter.
10. multistage direct evaporating-cooling unit according to claim 1, is characterized in that, described machine unit shell (1) outer circumferential is provided with some shutters (13) be connected with spray chamber (4).
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510003672.2A CN104613576A (en) | 2015-01-05 | 2015-01-05 | Multistage direct evaporation cooling machine set |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510003672.2A CN104613576A (en) | 2015-01-05 | 2015-01-05 | Multistage direct evaporation cooling machine set |
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| CN104613576A true CN104613576A (en) | 2015-05-13 |
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| CN201510003672.2A Pending CN104613576A (en) | 2015-01-05 | 2015-01-05 | Multistage direct evaporation cooling machine set |
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Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105698444A (en) * | 2016-03-18 | 2016-06-22 | 山东大学 | Air dehydrating and cooling pretreatment evaporation type condenser utilizing overheat refrigerant heat source |
| CN105783344A (en) * | 2016-03-18 | 2016-07-20 | 山东商业职业技术学院 | Air dehumidification cooling pretreatment evaporation condenser using solar heat source |
| CN106642454A (en) * | 2016-12-02 | 2017-05-10 | 艾科尔新能源科技有限公司 | Cooling capacity reducing type evaporative-condensation air conditioner and application method thereof |
| CN108507233A (en) * | 2017-09-19 | 2018-09-07 | 约克广州空调冷冻设备有限公司 | A kind of heat-exchange system |
| CN109899952A (en) * | 2019-03-14 | 2019-06-18 | 马克宁 | Double evaporation energy-saving air-conditioner sets |
| CN111359251A (en) * | 2020-04-14 | 2020-07-03 | 杭州蕴泽环境科技有限公司 | High-humidity flue gas grading condensation and dehumidification device and method |
| CN111405808A (en) * | 2020-02-27 | 2020-07-10 | D·盖达斯珀 | Circulating fluidized bed atomization drying cooler of electric automobile |
| CN111905518A (en) * | 2020-08-03 | 2020-11-10 | 珠海格力电器股份有限公司 | High-reliability purification device, negative pressure water chilling unit and control method |
| CN112128895A (en) * | 2020-09-30 | 2020-12-25 | 江苏鸿辉能源工程有限公司 | Air conditioning ventilation and water cooling system for workshop clean room |
| CN112857081A (en) * | 2021-03-29 | 2021-05-28 | 北京中热信息科技有限公司 | Low-noise spray-type evaporative cooling heat exchanger |
| EP3936216A1 (en) * | 2020-09-04 | 2022-01-12 | Chen-Hsin Lin | Swirl air/liquid air purifier |
| CN114122455A (en) * | 2021-11-19 | 2022-03-01 | 上海青氢科技有限公司 | Fuel cell engine air system |
| WO2022271095A3 (en) * | 2021-06-01 | 2023-03-23 | Pak Chuen Chang | An apparatus and a method for simulating one or more eco habitat conditions |
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Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105783344A (en) * | 2016-03-18 | 2016-07-20 | 山东商业职业技术学院 | Air dehumidification cooling pretreatment evaporation condenser using solar heat source |
| CN105783344B (en) * | 2016-03-18 | 2018-03-30 | 山东商业职业技术学院 | Utilize the air dewetting cooling pretreatment evaporative condenser of solar source |
| CN105698444A (en) * | 2016-03-18 | 2016-06-22 | 山东大学 | Air dehydrating and cooling pretreatment evaporation type condenser utilizing overheat refrigerant heat source |
| CN106642454A (en) * | 2016-12-02 | 2017-05-10 | 艾科尔新能源科技有限公司 | Cooling capacity reducing type evaporative-condensation air conditioner and application method thereof |
| CN108507233B (en) * | 2017-09-19 | 2023-09-29 | 约克广州空调冷冻设备有限公司 | Heat exchange system |
| CN108507233A (en) * | 2017-09-19 | 2018-09-07 | 约克广州空调冷冻设备有限公司 | A kind of heat-exchange system |
| CN109899952A (en) * | 2019-03-14 | 2019-06-18 | 马克宁 | Double evaporation energy-saving air-conditioner sets |
| CN111405808A (en) * | 2020-02-27 | 2020-07-10 | D·盖达斯珀 | Circulating fluidized bed atomization drying cooler of electric automobile |
| CN111359251A (en) * | 2020-04-14 | 2020-07-03 | 杭州蕴泽环境科技有限公司 | High-humidity flue gas grading condensation and dehumidification device and method |
| CN111905518A (en) * | 2020-08-03 | 2020-11-10 | 珠海格力电器股份有限公司 | High-reliability purification device, negative pressure water chilling unit and control method |
| CN111905518B (en) * | 2020-08-03 | 2024-05-03 | 珠海格力电器股份有限公司 | High-reliability negative pressure water chilling unit and control method |
| EP3936216A1 (en) * | 2020-09-04 | 2022-01-12 | Chen-Hsin Lin | Swirl air/liquid air purifier |
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